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CONDUCTION Problem Set Alejandro, Jan Rannel Granada, Gat Hendrix, Jamie Salcedo, Angel Frances Villaflor, Kaye
STEADY STATE APPLICATIONS 5. The following data was obtained in a test on a flat-walled furnace, the linings of which consist of a 11.5 cm. non-corrosive brick of unknown conductivity and the outer wall of 20 cm clay brick, also of unknown conductivity. The temperature of the inner wall (flame side) was found to be 735°C and that of the outer wall 185°C. This furnace was lagged with 5 cm of magnesia (k=0.07 W/mK) thermocouples inserted at various points and the ff. data taken: Calculate the percentage of heat loss that is saved by the lagging. 88°C Temp of the outer surface of magnesia  475°C  Temp at the junction of ordinary brick and magnesia  700°C  Temp at the junction of brick layers  735°C  Temp of inner wall (flame side)
STEADY STATE APPLICATIONS Magnesia
Solution: Basis: Am = 1m2  From the data of composition with magnesia: q = ∆T/R R = ∆x/(km)(Am) q = ∆T(km)(Am)/ ∆x Series: q1 = q2 = q3 =qtotal q of magnesia(q3) =  (475-88)K(0.07W/mK)( 1m2)  = 541.8 W  0.05m q of magnesia = q of non-corrosive brick =  q of clay brick = q total = 541.2 W km = q(∆x)/(∆T)(Am) km of non-corrosive brick = (541.8W)(0.115m)/(735-700)( 1m2) = 1.7802 W/mK km of clay brick = (541.8 W)(0.20m)/(700-475) ( 1m2) = 0.4816 W/mK non-corrosive brick  clay brick  Magnesia  735°C  700°C  475°C  88°C
Using the data in the composition without the magnesia: Series: Rtotal = R1 + R2 + R3… Getting the R: R = ∆x/(km)(Am) R non-corrosive brick = (0.115m) /(1.7802 W/mK) ( 1m2) = 0.06460 K/W R of clay brick = (0.20m)/(0.4816 W/mK)( 1m2) = 0.4153 K/W Rtotal = 0.4799K/W q total = (735-185)K/(0.4799 K/W) = 1146.07 W percentage of heat loss that is saved by the lagging: (q total without the magnesia – q total with magnesia)  x  100% q total without magnesia (1146.07W-541,8W)  x 100% = 52.73% 1146.07W  non-corrosive brick  clay brick  735°C  185°C
UNSTEADY STATE APPLICATIONS ,[object Object]
UNSTEADY STATE APPLICATIONS ,[object Object],Given: X = 2.5cm To = 16 oC h = 204 kJ/hm2K L = 5cm T = 93 oC α = 0.186 m2/s k = 38.0 W/mK  T1 = 315 oC
UNSTEADY STATE APPLICATIONS Solution: h = 204  _kJ_   x  1000J  x  1h___   = 56.67 W/m2K hm2K   1 kJ   3600 s X1 =  2.5/100  = 0.0125m 2 Y =  315 – 93  = 0.74   315 – 16 m =  k__  =   38.0 W/mK__________  = 53.64 hX1  56.67 W/m2K (0.0125m) From the Heisler Chart(Cylinder): X = 10.1 =  αt__  =  (0.186) t  t = 0.0085s   X12   (0.0125)2
 
Geankoplis Problem ,[object Object]
[object Object],Given : L = 10 ft = 0.3048m k = 15.23 W/mK Di = 0.25 in. = 6.35x10-3m Do = 0.40 in. = 0.01016m T1­ = 40oF = 4.44oC + 273K = 277.44K T2 = 80oF = 26.67oC + 273K = 299.67K
[object Object],Solution: X = r2 - r1 = (0.01016/2) – (6.35x10-3/2) =1.905x10-3m Dlm =  0.01016-6.35 x10-3­___  = 8.11x10-3 ln (0.1016/6.35x10-3) Am = πlDlm q =  T1 - T2  =  (299.67 – 277.44)K______ X__   1.905x10-3m________________  = 1380.16watts  or J/s kmAm 15.23W/mK[(π)(0.3048m)(8.11x10-3)]m2 q = 1380.16watts  or  J  x  1BTU  = 1.31 BTU/s   s  1055J
Geankoplis Problem ,[object Object]
[object Object],Given: X = 25.4mm = 0.0254m To = 10oC T = 121 cC  (X = 0,center) T1 = 177 cC h = 25.6 W/m2-K k = 0.69 W/m-K α =  5.85x10-4m2/h
[object Object],Solution: X1 = 0.0254/2 = 0.0127m Y =  T1 – T  =  177 – 121  = 0.34 T1 - To  177 – 10 m =  k__  =   0.69.0 W/mK__________  = 2.1 hX1  (25.6 W/m2K)(0..0127m) n =   0___  = 0 0.0127 From the Heisler Chart (Plate): X = 3.2 =  αt__  =  ( 5.85x10-4m2/h ) t  t = 0.88h x  3600s  = 3168s     X12   ( 0.0127 )2   1h
 

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Problem set 2 4b5

  • 1. CONDUCTION Problem Set Alejandro, Jan Rannel Granada, Gat Hendrix, Jamie Salcedo, Angel Frances Villaflor, Kaye
  • 2. STEADY STATE APPLICATIONS 5. The following data was obtained in a test on a flat-walled furnace, the linings of which consist of a 11.5 cm. non-corrosive brick of unknown conductivity and the outer wall of 20 cm clay brick, also of unknown conductivity. The temperature of the inner wall (flame side) was found to be 735°C and that of the outer wall 185°C. This furnace was lagged with 5 cm of magnesia (k=0.07 W/mK) thermocouples inserted at various points and the ff. data taken: Calculate the percentage of heat loss that is saved by the lagging. 88°C Temp of the outer surface of magnesia 475°C Temp at the junction of ordinary brick and magnesia 700°C Temp at the junction of brick layers 735°C Temp of inner wall (flame side)
  • 4. Solution: Basis: Am = 1m2 From the data of composition with magnesia: q = ∆T/R R = ∆x/(km)(Am) q = ∆T(km)(Am)/ ∆x Series: q1 = q2 = q3 =qtotal q of magnesia(q3) = (475-88)K(0.07W/mK)( 1m2) = 541.8 W 0.05m q of magnesia = q of non-corrosive brick = q of clay brick = q total = 541.2 W km = q(∆x)/(∆T)(Am) km of non-corrosive brick = (541.8W)(0.115m)/(735-700)( 1m2) = 1.7802 W/mK km of clay brick = (541.8 W)(0.20m)/(700-475) ( 1m2) = 0.4816 W/mK non-corrosive brick clay brick Magnesia 735°C 700°C 475°C 88°C
  • 5. Using the data in the composition without the magnesia: Series: Rtotal = R1 + R2 + R3… Getting the R: R = ∆x/(km)(Am) R non-corrosive brick = (0.115m) /(1.7802 W/mK) ( 1m2) = 0.06460 K/W R of clay brick = (0.20m)/(0.4816 W/mK)( 1m2) = 0.4153 K/W Rtotal = 0.4799K/W q total = (735-185)K/(0.4799 K/W) = 1146.07 W percentage of heat loss that is saved by the lagging: (q total without the magnesia – q total with magnesia) x 100% q total without magnesia (1146.07W-541,8W) x 100% = 52.73% 1146.07W non-corrosive brick clay brick 735°C 185°C
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  • 8. UNSTEADY STATE APPLICATIONS Solution: h = 204 _kJ_ x 1000J x 1h___ = 56.67 W/m2K hm2K 1 kJ 3600 s X1 = 2.5/100 = 0.0125m 2 Y = 315 – 93 = 0.74 315 – 16 m = k__ = 38.0 W/mK__________ = 53.64 hX1 56.67 W/m2K (0.0125m) From the Heisler Chart(Cylinder): X = 10.1 = αt__ = (0.186) t t = 0.0085s X12 (0.0125)2
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